EP0221598A2 - Metallische Trägerkatalysatoren und ihre Verwendung - Google Patents

Metallische Trägerkatalysatoren und ihre Verwendung Download PDF

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Publication number
EP0221598A2
EP0221598A2 EP86201809A EP86201809A EP0221598A2 EP 0221598 A2 EP0221598 A2 EP 0221598A2 EP 86201809 A EP86201809 A EP 86201809A EP 86201809 A EP86201809 A EP 86201809A EP 0221598 A2 EP0221598 A2 EP 0221598A2
Authority
EP
European Patent Office
Prior art keywords
catalyst
carrier
range
pbw
zirconium
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP86201809A
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English (en)
French (fr)
Other versions
EP0221598A3 (en
EP0221598B1 (de
Inventor
Krijn Pieter De Jong
Johannes Henrina Everardus Glezer
Martin Franciscus Maria Post
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
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Filing date
Publication date
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Priority to AT86201809T priority Critical patent/ATE60255T1/de
Publication of EP0221598A2 publication Critical patent/EP0221598A2/de
Publication of EP0221598A3 publication Critical patent/EP0221598A3/en
Application granted granted Critical
Publication of EP0221598B1 publication Critical patent/EP0221598B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
    • C07C1/0425—Catalysts; their physical properties
    • C07C1/043—Catalysts; their physical properties characterised by the composition
    • C07C1/0435—Catalysts; their physical properties characterised by the composition containing a metal of group 8 or a compound thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
    • C07C1/0485—Set-up of reactors or accessories; Multi-step processes
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/02—Boron or aluminium; Oxides or hydroxides thereof
    • C07C2521/04—Alumina
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • C07C2521/08—Silica
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/12—Silica and alumina
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
    • C07C2523/42—Platinum
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74—Iron group metals
    • C07C2523/745—Iron
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74—Iron group metals
    • C07C2523/75—Cobalt
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74—Iron group metals
    • C07C2523/755—Nickel
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with noble metals

Definitions

  • the invention relates to catalysts comprising a carrier on which as metal components iron, nickel or cobalt promoted by zirconium is supported.
  • the invention relates to a supported metal catalyst suitable for the preparation of hydrocarbons from carbon monoxide and hydrogen.
  • Catalysts often used for this purpose comprise one or more metals from the iron group supported on a carrier.
  • a very active catalyst system consists of cobalt supported on a carrier, especially a silica carrier, and, as promoter, zirconium.
  • the Fischer-Tropsch catalysts are suitably prepared by com­bining the active ingredients and the carrier, e.g. by pre­cipitating the metal on the carrier from an aqueous solution of the metal or, preferably, by impregnating the carrier material with a compound of the metal in the presence of a liquid.
  • kneading techniques may be applied, especially if it is intended to prepare catalysts to be used in slurry reactors. In all preparation procedures the liquid is removed from the composition, followed by calcination and reduction.
  • the impregnated metal compound is converted into one or more metal oxides.
  • the metal oxide(s) is reduced under formation of the metal.
  • the reduction is carried out in the presence of hydrogen usually at elevated temperatures, e.g. in the range of 200-300 °C. It has been observed that when using silica as carrier, in some cases in the compositions to be used as catalysts metal hydrosilicates occur, which do not exhibit catalytic activity. Because the reduction of these hydrosilicates is laborious, or requires severe conditions, it has been investigated whether the formation of the said hydrosilicates can be minimized, or that their removal can be facilitated.
  • the invention relates to a catalyst comprising a carrier on which as metal component iron, nickel, or cobalt promoted by zirconium is supported whereby the system in addition contains as promoter a noble metal from Group VIII of the Periodic Table.
  • the invention relates in particular to a catalyst suitable for the preparation of hydrocarbons from carbon monoxide and hydrogen, which catalyst comprises cobalt supported on a carrier and as promoters zirconium and a noble metal of Group VIII of the Periodic Table.
  • a preferred catalyst comprises cobalt together with zirconium and platinum or palladium as promoters, platinum being in particular preferred. Mixtures of two or more noble metal promoters may also be used, if desired.
  • the amounts of cobalt and promoters prevailing in the catalyst may vary, but conveniently the catalyst preparation is performed in such a manner that the ultimate catalyst contains from 5-40 pbw cobalt, 0.25-50 pbw and in particular 0.5-25 pbw of zirconium and 0.0001-5 pbw, in particular 0.001-1 pbw of noble metal promoters per 100 pbw of carrier.
  • the carrier material in the catalysts according to the invention suitably consists of silica, silica-alumina or alumina. It is preferred to use silica, which preferably consists of silica per se, although carrier material containing, in addition to SiO2, minor amounts of other materials such as alumina or alumina silicates may be used as well.
  • the invention further relates to a method for the preparation of a cobalt, zirconium and noble metal-containing catalyst as hereinbefore defined.
  • a preferred preparation method comprises the contacting of a porous carrier with a cobalt compound and with compounds of the promoters to be incorporated, in the presence of a liquid, e.g. water, followed by the removal of the liquid, e.g. by evaporation, calcination of the composition at elevated temper­atures and subsequent reduction in the presence of hydrogen.
  • the impregnation of the various metals in the carrier may proceed in successive steps or in a single treatment. Suitable calcination temperatures are in the range of 400-600 °C, preferably between 450 and 550 °C.
  • An advantage of the process according to the invention consists in that the reduction may be performed at a temperature which is substantially lower than that required in the reduction of catalysts that do not contain a promoter of a noble metal of Group VIII.
  • the reduction period adequate for the preparation of the catalysts according to the invention is significantly shorter than the period required in reducing calcined catalysts of the type known in the art.
  • Suitable reduction temperatures are in the range of 50-300 °C.
  • the reduction period may be between 30 minutes and 24 hours whereby it will be clear that if a relatively low temperature is selected, a relatively long reduction period will be required and vice versa.
  • the invention further relates to a process for the preparation of hydrocarbons by contacting a mixture of carbon monoxide and hydrogen with a cobalt, zirconium and noble metal-containing catalyst, as hereinbefore defined.
  • a cobalt, zirconium and noble metal-containing catalyst as hereinbefore defined.
  • a silica-comprising catalyst is used.
  • the feed for this process may have been obtained, for instance, from a heavy carbon-containing material such as coal by gasification, or from light hydrocarbons, such as natural gas by steam reforming or partial oxidation.
  • Preferred reaction conditions are temperatures in the range of 125-350 °C, in particular in the range of 175-275 °C and pressures in the range of from 0.5 to 15 MPa, in particular in the range of from 1 to 10 MPa.
  • a preferred embodiment of the process according to the invention consists in that the preparation of hydrocarbons from carbon monoxide and hydrogen is used as the first step in a two-step process for the preparation of middle distillates.
  • hydrocarbon product or at least that part of the product which has an initial boiling point above the final boiling point of the desired middle distillate fraction, is subjected to a catalytic hydrotreatment as the second step in the process.
  • the catalytic hydrotreatment is suitably carried out by contacting the hydrocarbon material from the first step at elevated temperatures and pressures and in the presence of hydrogen with a catalyst comprising one or more metals having hydrogenation activity, supported on a carrier.
  • a catalyst comprising one or more metals from Group VIII, supported on a carrier.
  • a catalyst is preferred comprising platinum on a carrier 13-15 %w of which contains of alumina and the rest of silica.
  • the preferred reaction conditions in the hydro­treatment are temperatures in the range of 175-400 °C, in particular in the range of 250-350 °C, a hydrogen partial pressure of 1 to 25 MPa, in particular of 2.5 to 15 MPa, a space velocity of 0.1-5 kg.l ⁇ 1.h ⁇ 1, in particular of 0.25-2 kg.l ⁇ 1.h ⁇ 1 and a hydrogen/oil ratio of 100-5000 Nl.kg ⁇ 1, in particular of 250-2500 Nl.kg ⁇ 1.
  • the invention is further illustrated with the following Example.
  • a spherical silica carrier with an internal surface area of 112 m/ml (bulk volume) and an external surface area of 15 cm/ml (bulk volume) was dried at 120 °C.
  • the carrier was immersed during 15 sec in a solution of cobalt nitrate in ethanol and subsequently dried and calcined at 500 °C.
  • the treatment comprising of immer­sion, drying and calcination was repeated.
  • the cobalt-loaded carrier was contacted with a solution of zirconium nitrate in water (pore volume impregnation).
  • the carrier now loaded with cobalt and zirconium was calcined at 500 °C.
  • the composition of the catalyst was 10 Co/0.9 Zr/100 SiO2, its internal surface area was 94 m/ml (bulk volume) and its external surface area 15 cm/ml (bulk volume).
  • catalyst 1 was loaded with platinum by pore volume impregnation with an aqueous solution of Pt(NH3)4(OH)2, followed by drying at 120 °C and calcining at 500 °C.
  • the composition of the catalyst was 0.1 Pt/10 Co/0.9 Zr/100 SiO2, its internal and external surface area were identical with those of catalyst 1.
  • Catalysts 1 and 2 were tested for the conversion of synthesis gas in a tubular reactor in which the catalyst was present in the form of a fixed bed with a bulk volume of 10 ml.
  • catalyst 2 was by far superior as regards space-time yield and synthesis gas conversion, and a lower rate of deactivation.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
EP86201809A 1985-11-08 1986-10-17 Metallische Trägerkatalysatoren und ihre Verwendung Expired - Lifetime EP0221598B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT86201809T ATE60255T1 (de) 1985-11-08 1986-10-17 Metallische traegerkatalysatoren und ihre verwendung.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB858527549A GB8527549D0 (en) 1985-11-08 1985-11-08 Supported metal catalysts
GB8527549 1985-11-08

Publications (3)

Publication Number Publication Date
EP0221598A2 true EP0221598A2 (de) 1987-05-13
EP0221598A3 EP0221598A3 (en) 1987-10-28
EP0221598B1 EP0221598B1 (de) 1991-01-23

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EP86201809A Expired - Lifetime EP0221598B1 (de) 1985-11-08 1986-10-17 Metallische Trägerkatalysatoren und ihre Verwendung

Country Status (16)

Country Link
US (1) US4857497A (de)
EP (1) EP0221598B1 (de)
JP (1) JP2556314B2 (de)
CN (1) CN1015358B (de)
AT (1) ATE60255T1 (de)
AU (1) AU586511B2 (de)
BR (1) BR8605505A (de)
CA (1) CA1284487C (de)
DE (1) DE3677136D1 (de)
ES (1) ES2020934B3 (de)
GB (1) GB8527549D0 (de)
IN (1) IN167707B (de)
MY (1) MY100338A (de)
NL (1) NL8602630A (de)
NZ (1) NZ218194A (de)
ZA (1) ZA868451B (de)

Cited By (9)

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US5073661A (en) * 1990-05-04 1991-12-17 Shell Oil Company Process for the preparation of hydrocarbons
US5102851A (en) * 1988-12-28 1992-04-07 Den Norske Stats Oljeselskap A.S. Supported catalyst for hydrocarbon synthesis
US5116879A (en) * 1988-12-28 1992-05-26 Den Norske Stats Oljeselskap A.S. Process using a supported catalyst for hydrocarbon synthesis
EP0579330A1 (de) * 1992-07-14 1994-01-19 Shell Internationale Researchmaatschappij B.V. Verfahren zur Distillation von Fischer-Tropsch-Produkten
US5371308A (en) * 1992-08-25 1994-12-06 Shell Oil Company Process for the preparation of lower olefins
WO2008075030A2 (en) 2006-12-19 2008-06-26 Bp Exploration Operating Company Limited Fischer-tropsch catalyst
KR100954205B1 (ko) * 2008-06-17 2010-04-21 울산과학대학 산학협력단 오존 탈취반응용 복합촉매의 제조방법
WO2013188862A1 (en) 2012-06-16 2013-12-19 Herrmann Robert P A fisher tropsch method for offshore production risers or oil and gas wells
EP2851916A1 (de) 2013-09-23 2015-03-25 Industrias Lorenzo, SA Anordnung aus Tastenschaltern mit programmierbarer Anzeige

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JP4857565B2 (ja) * 2005-01-27 2012-01-18 株式会社Ｉｈｉ フィッシャー・トロプシュ合成触媒とその製造方法
EP1976629A1 (de) * 2006-01-23 2008-10-08 Shell Internationale Research Maatschappij B.V. Hydrierkatalysator und seine verwendung zur hydrierung von fischer-tropsch-endprodukten
US8614158B2 (en) * 2008-02-29 2013-12-24 Schlumberger Technology Corporation Fischer-trospch and oxygenate synthesis catalyst activation/regeneration in a micro scale process
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5102851A (en) * 1988-12-28 1992-04-07 Den Norske Stats Oljeselskap A.S. Supported catalyst for hydrocarbon synthesis
US5116879A (en) * 1988-12-28 1992-05-26 Den Norske Stats Oljeselskap A.S. Process using a supported catalyst for hydrocarbon synthesis
US5073661A (en) * 1990-05-04 1991-12-17 Shell Oil Company Process for the preparation of hydrocarbons
EP0579330A1 (de) * 1992-07-14 1994-01-19 Shell Internationale Researchmaatschappij B.V. Verfahren zur Distillation von Fischer-Tropsch-Produkten
US5371308A (en) * 1992-08-25 1994-12-06 Shell Oil Company Process for the preparation of lower olefins
WO2008075030A2 (en) 2006-12-19 2008-06-26 Bp Exploration Operating Company Limited Fischer-tropsch catalyst
KR100954205B1 (ko) * 2008-06-17 2010-04-21 울산과학대학 산학협력단 오존 탈취반응용 복합촉매의 제조방법
WO2013188862A1 (en) 2012-06-16 2013-12-19 Herrmann Robert P A fisher tropsch method for offshore production risers or oil and gas wells
US9005554B1 (en) 2012-06-16 2015-04-14 Robert P. Herrmann Fischer tropsch method for offshore production risers or oil and gas wells
US9006297B2 (en) 2012-06-16 2015-04-14 Robert P. Herrmann Fischer tropsch method for offshore production risers for oil and gas wells
EP2851916A1 (de) 2013-09-23 2015-03-25 Industrias Lorenzo, SA Anordnung aus Tastenschaltern mit programmierbarer Anzeige

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DE3677136D1 (de) 1991-02-28
MY100338A (en) 1990-08-28
CA1284487C (en) 1991-05-28
ES2020934B3 (es) 1991-10-16
US4857497A (en) 1989-08-15
JP2556314B2 (ja) 1996-11-20
ATE60255T1 (de) 1991-02-15
NL8602630A (nl) 1987-06-01
NZ218194A (en) 1989-06-28
CN86107489A (zh) 1987-06-10
IN167707B (de) 1990-12-08
JPS62117630A (ja) 1987-05-29
AU6486286A (en) 1987-05-14
BR8605505A (pt) 1987-08-11
EP0221598A3 (en) 1987-10-28
EP0221598B1 (de) 1991-01-23
ZA868451B (en) 1987-06-24
GB8527549D0 (en) 1985-12-11
AU586511B2 (en) 1989-07-13
CN1015358B (zh) 1992-02-05

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